Patent Application
20060123816
This invention relates to vapor compression refrigeration systems and, more particularly, to vapor compression refrigeration systems having a flow regulating device with at least one spring positioned adjacent to a float.
As is commonly known, vapor compression refrigeration systems are used in refrigerators, freezers, air conditioners and heat pumps. Typically, vapor compression refrigeration systems include a compressor, a condenser, a drier/filter, a flow control device and an evaporator. In vapor compression refrigeration systems, a refrigerant such as R12 is compressed as a vapor in the compressor, cooled to a liquid in the condenser, passed through the flow control device and vaporized in the evaporator. The vaporization of refrigerant draws heat from around the evaporator so as to provide refrigeration.
The flow control device meters liquid refrigerant from the condenser into the evaporator at a rate commensurate with the rate at which vaporization occurs in the evaporator. The flow control device also attempts to maintain a pressure differential between high and low pressure sides of the vapor compression refrigeration system in order to permit the refrigerant to vaporize under a desired low pressure in the evaporator, while at the same time condensing at a high pressure in the condenser.
In the prior art, several different types of flow control device are used. One type of flow control device is a controlled expansion valve. A controlled expansion valve typically has a diaphragm or bellows that is movable in response to a signal received from a temperature sensor mounted in, or adjacent to, a condenser. Controlled expansion valves tend to be large and somewhat expensive. Accordingly, controlled expansion valves are typically used in large vapor compression systems.
Another type of flow control device is a float valve. A float valve typically includes a float that is disposed within a chamber and is movable in response to changes in the level of refrigerant in the chamber. Two examples of float valves include U.S. Pat. No. 3,103,106 to Tipton and U.S. Pat. No. 2,191,623 to Philipp, both of which are incorporated herein by reference. Tipton and Philipp each disclose a float valve having an inlet connected to a condenser and an outlet connected to a high side of an evaporator. The outlet is fitted with a valve seat. The float valve includes a housing that defines an inner chamber. The inlet passes through a top wall of the housing, while the outlet passes through a bottom wall of the housing. A float with a needle projecting downward therefrom is movably disposed in the chamber and is aligned with the valve seat. The float is supposed to move in accordance with changes in the level of refrigerant in the chamber. When the level of refrigerant is below a certain level, the needle moves into the valve seat and closes the outlet. When the level of refrigerant rises above the certain level, the float rises and the needle moves away from the valve seat, thereby opening the outlet. Such float valves, however, tend to be expensive to manufacture and their valve seats tend to have a relatively short life.
Of particular interest is U.S. Pat. No. 5,799,504 (herein incorporated by reference) which relates to vapor compression refrigeration system having a condenser, a regulating device, and a capillary tube. The regulating device has a housing defining an inner chamber for receiving refrigerant from the condenser. A float is disposed within the chamber and includes a resilient surface. An outlet line connected to the capillary tube extends through a bottom wall of the housing and into the chamber. The float is movable in response to changes in level of refrigerant in the chamber. The float moves downward to close the outlet line when refrigerant in the chamber drops below a minimum level, and is supposed to move upward to open the outlet line when refrigerant in the chamber rises above the minimum level.
In small vapor compression systems, such as domestic refrigerators, the most common flow control device is a capillary tube. Since the capillary tube has a fixed restriction, the capillary tube is sized for optimal efficiency at a single set of ambient and internal temperatures and pressures. Capillary tubes offer the advantages of low cost, high reliability, and the added efficiency of being easily placed in heat exchange relationship with a return line from the evaporator to the compressor.
Typically, a capillary tube is provided with only a moderate restriction, i.e., is sized relatively “loose”, in order to allow fast flooding of the evaporator when the compressor is turned on. The fast flooding of the evaporator allows the vapor compression system to quickly reach a high running efficiency, thereby reducing the amount of time the compressor must run. Once the evaporator is flooded, however, gaseous refrigerant from the condenser often passes through the capillary tube and into the evaporator. This gaseous refrigerant does not provide any refrigeration because it does not go through a phase change. The gaseous refrigerant, however, must still be handled by the compressor. Thus, the compressor may become loaded with an increased mass flow that does not refrigerate, which is inefficient. In addition, when the compressor is turned off, the pressure across the capillary is supposed to quickly equalize, forming flash gas in the capillary tube and allowing hot liquid refrigerant and hot gaseous refrigerant from the condenser to pass into the evaporator. Of course, this adds heat to the evaporator and further decreases the efficiency of the vapor compression system.
Some prior art vapor compression refrigeration systems utilize a regulating device to ameliorate the foregoing adverse effects of a loosely sized capillary tube. Two examples of such prior art vapor compression refrigeration systems having such regulating devices are U.S. Pat. No. 5,201,190 to Nelson et al. and U.S. Pat. No. 5,205,131 to Powlas, both of are incorporated herein by reference. Both Nelson and Powlas show a subcooling valve having a housing with an inlet connected to a condenser and an outlet connected to a capillary tube. The housing defines a first chamber wherein a bellows apparatus is disposed. The bellows apparatus is filled with non-system refrigerant and is movable in response to changes in the temperature and pressure of system refrigerant entering the subcooling valve. A valve member is connected to the bellows apparatus and is operable to open and close the outlet of the housing in response to movement of the bellows apparatus. When a compressor is running, the subcooling valve opens and closes in a modulating manner to allow only sub-cooled liquid refrigerant to enter the capillary tube. When the compressor stops, the subcooling valve closes to prevent any gaseous refrigerant from entering the capillary tube.
The subcooling valve shown in Nelson and Powlas can be affected by temperature or pressure changes in the subcooling valve that are not caused by temperature or pressure changes in the system refrigerant. In addition, the subcooling valve shown in Nelson and Powlas is a complex device that is relatively expensive to manufacture.
There is a need in the art for a vapor compression refrigeration system that ameliorates the adverse effects of a sunken or partially submerged float due to a high differential pressure in a refrigeration system, deals with the adverse effects of a loosely sized capillary tube, is inexpensive to manufacture, and is not affected by temperature or pressure. The present invention is directed to such a vapor compression refrigeration system.
Accordingly, it is an objective of the present invention to provide a vapor compression refrigeration system having a regulating device that ameliorates the adverse effects of a partially submerged float.
It is another objective of the present invention to provide a vapor compression refrigeration system having a regulating device that ameliorates the adverse effects of a completely submerged float.
It is another objective of the present invention to ameliorate the adverse effects of a float sticking to an outlet tube.
It is another object of the present invention to compensate differential pressure build up in vapor compression refrigeration systems.
It is another object of the present invention to eliminate the adverse effects of a loosely sized capillary tube in state-of-the-art vapor compression refrigeration systems.
It is another object of the present invention to provide a vapor compression refrigeration system that is inexpensive to manufacture and is not affected by temperature or pressure.
These and other objective of the present invention are met by providing a refrigeration valve device comprising: a housing having a top wall, a side wall, and a bottom wall defining an inner chamber, a float disposed within the chamber; and at least one spring positioned between the float and the housing. Preferably the spring is a coil. Optionally, the spring is a compression spring, or a conical spring. Preferably, the housing comprises an inlet portion and an outlet portion and the spring is positioned between the float and the outlet portion. Preferably, the float has a generally planar bottom surface. Preferably, a resilient pad is secured to the bottom surface of the float. Optionally, the spring has a top end and a bottom end, and the top end is mounted to the float around the resilient pad. Optionally, the housing further comprises an inlet portion and an outlet portion, and the spring has a bottom end mounted around the outlet portion. Optionally, the valve device further comprises a filter assembly disposed within the inner chamber between the top wall and the float. Optionally, the valve device comprises a plate disposed within the chamber between the top wall and the float. Optionally, the side wall is substantially cylindrical, and the plate is substantially circular. Optionally, the plate adjoins the side wall of the housing and defines at least one perforation through the plate. Optionally the valve device comprises a screen disposed within the chamber between the plate and the float. Optionally the valve device further comprises a desiccant material disposed with the chamber between the screen and the plate. Optionally, the plate is spaced inward from the side wall of the housing so as to form an annular gap between the sidewall and the plate. Optionally, the float is disposed radially inward of the gap. Optionally, the valve device further comprises a flow control device connected to the housing. Preferably, the flow control device is a capillary tube. Optionally, the valve device comprises a float further comprising an inner core covered by an outer shell, the outer shell comprising a resilient surface. Preferably, such a float is substantially spherical and made of rubber. Optionally, the valve device may have a plurality of springs positioned between the float and the housing. Preferably, the valve device is disposed within a refrigeration system comprising: an evaporator for vaporizing refrigerant to provide cooling; a compressor for drawing refrigerant from the evaporator; a condenser for condensing refrigerant from the compressor; and a flow control device for maintaining pressure drop between the condenser and the evaporator, where the flow control device has an inlet portion and an outlet portion, the outlet portion being connected to the evaporator. Preferably, the valve is positioned in the refrigeration system between the condenser and the flow control device.
The objectives of the present invention are further met by providing are method of offsetting differential pressure in a refrigeration system comprising positioning a refrigeration valve within the refrigeration system wherein the refrigeration valve comprises a housing having a top wall, a side wall, and a bottom wall defining an inner chamber, a float disposed within the chamber; and at least one spring between the float and the housing. Preferably, the refrigeration system further comprises: an evaporator for vaporizing refrigerant to provide cooling; a compressor for drawing refrigerant from the evaporator; a condenser for condensing refrigerant from the compressor; and a flow control device for maintaining pressure drop between the condenser and the evaporator, the flow control device having an inlet portion and an outlet portion, the outlet portion being connected to the evaporator. Preferably, the refrigeration valve is positioned between the condenser and the flow control device. Optionally, the spring is a coil, compression, or conical spring. Optionally, the housing further comprises an inlet portion and an outlet portion and the spring is positioned between the float and the outlet portion. Optionally, the float has a generally planar bottom surface. Preferably, a resilient pad secured to the bottom surface. Preferably the method comprises a filter assembly disposed within the inner chamber between the top wall and the float. Optionally, the float further comprises an inner core covered by an outer shell, the outer shell comprising a resilient surface. Optionally, the float is substantially spherical.
It should be noted that in the detailed description which follows, identical components have the same reference numerals, regardless of whether they are shown in different embodiments of the present invention. It should also be noted that in order to clearly and concisely disclose the present invention, the drawings may not necessarily be to scale and certain features of the invention may be shown in somewhat schematic form.
Float systems such as those described in U.S. Pat. No. 5,799,504 do not function properly under normal system operations due to a high differential pressure buildup in the system. The high differential pressure results in a net force which may hold the float against the outlet tube preventing the float from floating, cause the float to stick to the outlet tube delaying the float from floating when refrigerant is added, or generally decrease efficiency of the system. These situations are problematic for refrigerant may be prevented from flowing smoothly through the system. When the float is held against the outlet, systemic failure may occur for the system may clog such that no refrigerant is able to circulate throughout the system. When the float sticks to the outlet, more liquid refrigerant than normally required must build up in the regulating device in order to buoy the float. A sticking float may cause inefficient delay in the system, and may stress other parts of the refrigeration system such as the compressor. When the system has to work harder more energy is needed to run the system which may also increase operation costs. Accordingly, the detrimental effects of the high differential pressure on the entire refrigeration system may be extensive. Any break or clog in a system may either decrease efficiency or cause systemic failure. The inclusion of a spring in a float valve has been found to compensate or offset the high differential pressure, thus eliminating the problems associated therewith.
Also, in state-of-the-art systems where capillary tubes are positioned adjacent to a float valve, the high differential pressure may cause the float to stick or clog the tube, which may prevent refrigerant from flowing into the capillary tube. Accordingly, no fast flooding of the evaporator can occur when the compressor is turned on. However, it has now been found that the inclusion of a spring in a float valve promotes fast flooding of the evaporator.
Referring now to
The refrigeration system 20 is a closed recirculating system filled with a suitable refrigerant such as R12 or R134a. The vapor compression system generally includes an electric motor-driven compressor 22, a condenser 24, a capillary tube 26, an evaporator 28 and float valve 100 embodied in accordance with the present invention. The evaporator 28 is mounted inside an insulated compartment 15 within the refrigerator, whereas the compressor 22 and the condenser 24 are mounted external to the insulated compartment 15.
The compressor 22 withdraws vaporized refrigerant from the evaporator 28 through a suction line 30 and discharges hot compressed refrigerant to the condenser 24 through a discharge line 32. The compressed refrigerant condenses to a liquid in the condenser 24 and discharges its heat to the outside environment. From the condenser 24, the liquid refrigerant passes through a valve line 36 and then the float valve 100. After the float valve 100, the liquid refrigerant passes through an outlet line 39 and then the capillary tube 26. The capillary tube 26 maintains a pressure drop between the condenser 24 and the evaporator 28. The pressure drop causes the refrigerant to vaporize in the evaporator 28. The vaporization of the refrigerant in the evaporator 28 draws heat from the insulated compartment 15, thereby cooling or refrigerating the insulated compartment 15.
In order to maintain the insulated compartment 15 at a desired temperature, a sensing bulb 50 is mounted within the insulated compartment 15 and is connected to a thermostat 60. The sensing bulb 50 provides a signal representative of the temperature in the insulated compartment 15 to the thermostat 60. The thermostat 60 is provided with contacts (not shown in
The length of time the compressor 22 runs, i.e., its duty cycle, depends upon numerous factors such as the ambient temperature surrounding the insulated compartment 15, the thermal mass disposed within the insulated compartment 15, and the number of times an access door is opened to allow the admission of warmer outside air. The refrigeration system 20 is sized to so that under most conditions, the compressor 22 will have a duty cycle of approximately fifty percent.
Since the duty cycle of the compressor 22 is approximately fifty percent, the capillary tube 26 is sized “loose”, i.e., with a reduced restriction, which allows fast flooding of the evaporator 28 when the compressor 22 is started. Although not shown, the capillary tube 26 is connected so as to be in thermal contact with the suction line 30. The suction line 30 cools the capillary tube 26.
Referring now to
The top segment 111 includes the top side wall 113a, a top wall 112 and an open bottom end. The top side wall 113a has a flared portion at the bottom end. An annular ridge 114 is formed into the top wall 112 and extends downward therefrom. The top wall 112 defines a top opening 120 within which an end of the valve line 36 is securely disposed.
The bottom segment 115 includes the bottom sidewall 113b, a bottom wall 116 and an open top end. The bottom wall 116 defines a bottom opening 122. A spring 123 is fixed around bottom opening 123. A portion of the outlet line 39 is secured within the bottom opening 122. The outlet line 39 extends into the chamber 130 through the bottom opening 122 and terminates at an open interior end spaced above the bottom wall 116 and within spring 123. Spring 123 is positioned below and adjacent to float 150.
Spring 123 is of considerable importance because it surprisingly improved the performance of float valve 100. This is especially true in sequential combination between float 150 and bottom wall 116. Similar float valves not having a spring or biasing means positioned between float and outlet line do not function well due to a high differential pressure that occurs in normal system operation. The high differential pressure results in a net force holding the float against the outlet, thus preventing the float from floating correctly. Such floats tend to stick decreasing efficiency of the unit, or worse clog the unit causing systemic failure. Referring back to
Spring 123 may be made out of any material that one of ordinary skill in the art would use to make a spring. Spring 123 can be composed of plastic, thin steel, or other type of material or combination thereof such as metal and polymer or metal coated with a polymer. Polymer coated metallic springs are preferred since they resist corrosion when placed in contact with water. Spring 123 may be any type of spring that when a load is applied thereto will deflect spring 123 and removing the load will cause the spring to return to its previous position. Accordingly, spring 123 has shape retentive qualities. Spring 123 is positioned in order to be capable of moving float 150 away from bottom opening 122, when spring 123 has been deflected or compressed due to the load of float 150 and/or differential pressure in the system. Spring 123 is preferably a coil type compression spring. Such compression springs are typically made from a length of usually round steel wire that is formed into a series of loops that allow for movement to take place. The metal may be coated with a polymer. Although coil springs are the preferred embodiment, one of ordinary skill in the art can appreciate that spring 123 may be any type of spring including a torsion spring, leaf spring, or conical spring.
Referring to
Referring to
Referring back to
A filter assembly is disposed within the chamber 130 toward the top wall 112 of the canister 110. The filter assembly is comprised of a drier 142 disposed between a dispersal plate 144 and a screen plate 146.
The dispersal plate 144 is disposed adjacent to, but is spaced downward from, the top wall 112 by the ridge 114. The dispersal plate 144 is substantially circular and is sized to have a diameter slightly larger than the diameter of the chamber 130. In this manner, the dispersal plate 144 can be friction fit inside the chamber 130. The dispersal plate 144 is composed of a rigid material such as steel or high impact plastic and has a plurality of perforations formed therein. The perforations permit refrigerant to flow through the dispersal plate 144. The perforations, however, do not allow large particulate contaminants in the refrigerant to pass through the dispersal plate 144. The perforations are spread out over substantially all of the dispersal plate 144 so as to disperse refrigerant flowing downward through the dispersal plate 144. Thus, the dispersal plate 144 both filters and disperses the refrigerant.
The drier 142 is composed of a desiccant material such as synthetically produced crystalline metal alumino-silicates. The drier 142 removes water as well as other contaminants that may be present in the refrigerant. The drier 142 is packed into the chamber 130 below the dispersal plate 144 and is held in place by the screen plate 146.
The screen plate 146 is comprised of a screen 148 surrounded by an outer ring 147. The screen 148 is a very fine steel mesh that will permit refrigerant but not the desiccant material of the drier 142 to flow therethrough. The outer ring 147 is composed of a rigid material such as steel or high impact plastic and is sized to have a diameter slightly larger than the diameter of the chamber 130. In this manner, the screen plate 146 can be friction fit inside the chamber 130.
As shown in
Spring 123 is positioned between pad 160 and aligned with the interior end of the outlet line 39. Spring 123 may be attached to either bottom end wall 156 or bottom wall 116, however is preferably attached as shown to bottom wall 116.
A plurality of upper pins 170 and a plurality of lower pins 172 extend radially inward from the side wall 113 of the canister 110. The upper pins 170 and lower pins 172 terminate at free ends spaced radially outward from the side wall 152 of the float 150. The upper pins 170 are secured to the top side wall 113a and are evenly disposed around the circumference thereof. The lower pins 172 are secured to the bottom side wall 113b and are evenly disposed around the circumference thereof. The upper and lower pins 170, 172 guide the float 150 inward, away from the side wall 113 so as to prevent the float 150 from adhering to the side wall 113.
It should be appreciated that the upper and lower pins 170, 172 can be secured to the side wall 152 of the float 150, instead of the top side wall 113a and the bottom side wall 113b of the canister 110. Moreover, the upper and lower pins 170, 172 can be replaced with annular rings that are formed in the top side wall 113a and the bottom side wall 113b, and that extend radially inward therefrom. Alternately, the upper and lower pins 170, 172 can be replaced with bumps or ridges that are formed in the side wall 152 of the float 150.
When the compressor 22 is off, and has not been run for some time, the level of liquid refrigerant in the chamber 130 is below a minimum level. As a result, the float 150 is supported by the interior end of the outlet line 39, with the pad 160 disposed therebetween.
When the compressor 22 is started, the compressor 22 pumps residual refrigerant out of the evaporator 28 and into the condenser 24, thereby causing an increase in pressure inside the condenser 24. This increase in pressure causes refrigerant to flow out of the condenser 24 and into the valve line 36. Refrigerant in the valve line 36 flows to the float valve 100 and enters the chamber 130 through the top opening 120. A high differential pressure is problematic in that it causes pad 160 to stick or clog outlet 39. Spring 123 overcomes this pressure as refrigerant flows downward.
Refrigerant flows downward from the top opening 120 in a concentrated stream and strikes the dispersal plate 144. The dispersal plate 144 breaks up the concentrated stream and spreads the refrigerant out over substantially all of the dispersal plate 144. Refrigerant flows through the dispersal plate 144 and into the drier 142. Any large particulate contaminants that are present in the refrigerant are deposited on the dispersal plate 144. As refrigerant passes through the drier 142, the drier 142 removes water that may be present in the refrigerant. Other impurities in the refrigerant, such as metal particulates, are also removed by the drier 142. In this manner, the drier 142 filters as well as dries the refrigerant.
From the drier 142, refrigerant passes through the screen plate 146 and flows downward onto the float 150. Refrigerant runs off the float 150 and accumulates at the bottom wall 116. As refrigerant continues to flow into the chamber 130, the level of refrigerant in the chamber 130 rises. When the level of refrigerant rises above the minimum level, which is above the interior end of the outlet line 39, the refrigerant in combination with the force from spring 123 buoys the float 150 upward and lifts the pad 160 off the interior end, thereby opening the outlet line 39. As a result, refrigerant from the chamber 130 flows through the outlet line 39 and travels to the capillary tube 26. Refrigerant flows through the capillary tube 26 and vaporizes in the evaporator 28 to provide refrigeration to the insulated compartment 15.
As the compressor 22 continues running, the temperature of the insulated compartment 15 and the evaporator 28 drops. As a result, the total mass flow of liquid refrigerant in the refrigeration system 20 drops, thereby causing the level of liquid refrigerant in the chamber 130 to drop. However, the float valve 100 will keep the outlet line 39 open as long as liquid refrigerant in the chamber 130 remains above the minimum level, and as long as spring 123 overcomes any forces which may cause it float 150 to stick or clog. If the level of liquid refrigerant drops below the minimum level, the float valve 100 will compress spring 123 and close the outlet line 39. Thus, the level of liquid refrigerant in the chamber 130 will always be above the interior end when the float valve 100 opens the outlet line 39. In this manner, the float valve 100 prevents vaporized refrigerant from passing through the float valve 100 to the capillary tube 26.
It should be appreciated that the dispersal plate 144 helps maintain the proper operation of the float valve 100 when the compressor 22 is running and liquid refrigerant is flowing downward into the chamber 130. The dispersal plate 144 disperses the concentrated stream of refrigerant entering the chamber 130. This dispersal prevents the concentrated stream from directly impinging upon the float 150 and forcing the float 150 to move downward.
When the compressor 22 stops running for any reason, such as by operation of the thermostat 60 detecting the lower predetermined temperature in the insulated compartment 15, the compressor 22 stops pumping refrigerant into the condenser 24. As a result, refrigerant substantially stops flowing into the chamber 130 of the float valve 100. However, refrigerant continues to flow out of the chamber 130 because there is still a pressure differential across the capillary tube 26. Thus, the level of refrigerant in the chamber 130 drops. When the level of refrigerant in the chamber 130 drops below the minimum level, the refrigerant no longer buoys the float 150 upward above the interior end, and the float 150 once again compresses spring 123 and presses the pad 160 against the interior end, thereby closing the outlet line 39. With the outlet line 39 closed, vaporized or liquid refrigerant from the condenser 24 cannot enter the capillary tube 26 and the evaporator 28. Since the float valve 100 prevents hot vaporized or liquid refrigerant from entering the evaporator 28 when the compressor 22 is off, the float valve 100 prevents heating of the evaporator 28, and hence the insulated compartment 15, that would otherwise occur if the float valve 100 was not present.
In addition to stopping the flow of hot vaporized or liquid refrigerant to the evaporator, the float valve 100 helps maintain a pressure differential within the refrigeration system 20 when the compressor 22 is off. This pressure differential enables the evaporator 28 to flood quicker when the compressor 22 is restarted. As a result, running conditions are more quickly re-established, thereby decreasing the run time of the compressor 22 for a given amount of cooling. Spring 123 overcomes any negative effects of the differential pressure on float 150 such as sticking or clogging.
Referring now to
The deflector plate 182 is composed of a rigid material such as steel or high impact plastic and has a pair of holes 183 formed therein. Each of the projections 186 is substantially cylindrical and has a bore extending partially therethrough. The deflector plate 182 is disposed adjacent to the projections 186 such that the holes 183 are aligned with the bores. A pair of screws 188 are threaded through the holes 183 and bores so as to secure the deflector plate 182 to the top wall 112 in a spaced-apart arrangement. The deflector plate 182 is substantially circular and is sized to have a diameter smaller than the diameter of the chamber 130. Thus, an annular gap 80 is formed between the deflector plate 182 and the side wall 113. The deflector plate 182, however, is sized to have a diameter slightly larger than the diameter of the float 150 so the float 150 can be disposed radially inward of the gap 80. In this manner, the deflector plate 182 fully shields the float 150 from above.
When the compressor 22 is running and the concentrated stream of liquid refrigerant is flowing downward into the chamber 130, the deflector plate 182 disperses the concentrated stream and directs the refrigerant toward the annular gap 80. The refrigerant flows through the annular gap 80 and falls toward the bottom wall 116. Most of the refrigerant passes between the float 150 and the side wall 113 as it falls downward. Thus, in addition to dispersing the concentrated stream of refrigerant, the deflector plate 182 also directs the refrigerant away from the float 150. In this manner, the deflector plate 182 substantially prevents refrigerant from directly contacting the float 150.
Referring now to
As shown in
The float 192 operates in a manner similar to the float 150. When the compressor 22 is off, and has not been run for some time, the level of liquid refrigerant in the chamber 130 is below a minimum level. As a result, the float 192 compresses spring 123 and rests on the interior end of the outlet line 39 as is shown in
When the compressor 22 is started, liquid refrigerant flows from the condenser 24, through the valve line 36 and enters the chamber 130 through the top opening 120. When the level of refrigerant rises above the minimum level, the refrigerant and spring 123 buoys the float 192 upward and lifts the outer shell 196 off the interior end of the outlet line 39, thereby opening the outlet line 39. As. a result, refrigerant from the chamber 130 flows through the outlet line 39 and travels to the capillary tube 26.
When the compressor 22 stops running for any reason, the level of refrigerant in the chamber 130 drops. When the level of refrigerant in the chamber 130 drops below the minimum level, the refrigerant no longer buoys the float 192 upward above the interior end, and the outer shell 196 once again is pressed against the spring, and interior end, thereby closing the outlet line 39. With the outlet line 39 closed, vaporized or liquid refrigerant from the condenser 24 cannot enter the capillary tube 26 and the evaporator 28. When high differential pressure causes float 192 to stick or clog outlet line 39, spring 123′ urges the float off of outlet line 39.
It should be appreciated that the generally spherical shape of the float 192 greatly decreases the amount of surface area of the float 192 that can contact the side wall 113 of the canister 110 at any one time. This reduction in surface area greatly reduces the amount of friction that develops between the float 192 and the side wall 13, and which impedes vertical movement of the float 192. Consequently, the need to guide the float 192 inward, away from the side wall 13, is eliminated, thereby permitting the upper pins 170 and the lower pins 172 to be removed from the canister 110.
The generally spherical shape of the float 192 permits the float 192 to rotate within the chamber 130. The rotation of the float 192, however, does not affect the operation of the float 192 because any portion of the outer shell 196 can compress spring 123 and close the interior end of the outlet line 39.
The present invention further includes methods of offsetting differential pressure in a refrigeration system comprising positioning refrigeration float valves as described herein within a refrigeration system. The inclusion of a spring in such float valves compensates the high differential pressure by nudging the float as described herein away from the outlet line and/or capillary tube.
Although the preferred embodiments of this invention have been shown and described, it should be understood that various modifications and rearrangements of the parts may be resorted to without departing from the scope of the invention as disclosed and claimed herein. For example, the canister 110 can be provided with a generally elliptical shape or a generally rectangular shape instead of a generally cylindrical shape. In the float valve 100 and the float valve 190, the outlet line 39 can be eliminated and the capillary tube 26 brought directly into the chamber 130 through the bottom opening 122, as is shown for the float valve 180. The spring may be a conical spring or other workable type or shape.
